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Catalysis of Organic..

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120TEMPO Oxidation <strong>of</strong> Alcoholsthe use <strong>of</strong> hypohalites very frequently leads to the formation <strong>of</strong> undesirablehalogenated by-products thus necessitating further purification <strong>of</strong> the oxidationproduct. Extensive review <strong>of</strong> TEMPO based oxidation methods can be found in theliterature (10,11,12) and the industrial application <strong>of</strong> a highly efficient solvent- andbromide-free system has been reported (13,14).In recent years, much effort has been spent on developing both selective andenvironmentally friendly oxidation methods using either air or oxygen as theultimate, oxidant. One <strong>of</strong> the most selective and efficient catalyst systems reported todate is based on the use <strong>of</strong> stable nitroxyl radicals as catalysts and transition metalsalts as co-catalysts (15). The most commonly used co-catalysts are (NH 4 ) 2 Ce(NO 3 ) 6(16), CuBr 2 -2,2’-bipiridine complex (17), RuCl 2 (PPh 3 ) 3 (18,19), Mn(NO 3 ) 2 -Co(NO 3 ) 2 and Mn(NO 3 ) 2 -Cu(NO 3 ) 2 (20). However, from an economic andenvironmental point <strong>of</strong> view, these oxidation methods suffer from one commondrawback. They depend on substantial amounts <strong>of</strong> expensive and/or toxic transitionmetal complexes and some <strong>of</strong> them require the use <strong>of</strong> halogenated solvents likedichloromethane, which makes them unsuitable for industrial scale production.XScheme 1.3 N . O(1mol%)HH H+ O+ H 2 O2OOHNBS (1mol%)1 2Mg(NO 3 ) 2 , (1mol%)40-50 o C, 40-50psi, AcOHX = H, TEMPO (3); X = OCH 3 , MeO-TEMPO (4); X = NHCOCH 3 , AATEMPO (5)Very recently, Hu et al. claimed to have discovered a convenient procedure forthe aerobic oxidation <strong>of</strong> primary and secondary alcohols utilizing a TEMPO basedcatalyst system free <strong>of</strong> any transition metal co-catalyst (21). These authors employeda mixture <strong>of</strong> TEMPO (1 mol%), sodium nitrite (4-8 mol%) and bromine (4 mol%) asan active catalyst system. The oxidation took place at temperatures between 80-100 °C and at air pressure <strong>of</strong> 4 bars. However, this process was only successful withactivated alcohols. With benzyl alcohol, quantitative conversion to benzaldehydewas achieved after a 1-2 hour reaction. With non-activated aliphatic alcohols (suchas 1-octanol) or cyclic alcohols (cyclohexanol), the air pressure needed to be raisedto 9 bar and a 4-5 hour <strong>of</strong> reaction was necessary to reach complete conversion.Unfortunately, this new oxidation procedure also depends on the use <strong>of</strong>dichloromethane as a solvent. In addition, the elemental bromine used as a cocatalystis rather difficult to handle on a technical scale because <strong>of</strong> its high vaporpressure, toxicity and severe corrosion problems. Other disadvantages <strong>of</strong> this systemare the rather low substrate concentration in the solvent and the observed formation<strong>of</strong> bromination by-products.

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